CN107177581B - 一种改造腈水合酶及其应用 - Google Patents
一种改造腈水合酶及其应用 Download PDFInfo
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- CN107177581B CN107177581B CN201710456875.6A CN201710456875A CN107177581B CN 107177581 B CN107177581 B CN 107177581B CN 201710456875 A CN201710456875 A CN 201710456875A CN 107177581 B CN107177581 B CN 107177581B
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- Prior art keywords
- nitrile hydratase
- amino acid
- modified nitrile
- acrylamide
- modified
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- 108010024026 Nitrile hydratase Proteins 0.000 title claims abstract description 89
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 claims description 38
- 108090000623 proteins and genes Proteins 0.000 claims description 27
- 238000000034 method Methods 0.000 claims description 14
- 241000316848 Rhodococcus <scale insect> Species 0.000 claims description 11
- 150000001413 amino acids Chemical class 0.000 claims description 10
- 239000013604 expression vector Substances 0.000 claims description 7
- 238000004519 manufacturing process Methods 0.000 claims description 7
- 241000894006 Bacteria Species 0.000 claims description 6
- 241000588724 Escherichia coli Species 0.000 claims description 4
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 claims description 2
- 241000186216 Corynebacterium Species 0.000 claims description 2
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- 239000001110 calcium chloride Substances 0.000 claims description 2
- 229910001628 calcium chloride Inorganic materials 0.000 claims description 2
- 210000000349 chromosome Anatomy 0.000 claims description 2
- 238000004520 electroporation Methods 0.000 claims description 2
- 125000003275 alpha amino acid group Chemical group 0.000 claims 6
- XBDQKXXYIPTUBI-UHFFFAOYSA-M Propionate Chemical compound CCC([O-])=O XBDQKXXYIPTUBI-UHFFFAOYSA-M 0.000 claims 1
- 108090000790 Enzymes Proteins 0.000 abstract description 16
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Abstract
本发明公开了属于酶工程和工业微生物技术领域的一种改造腈水合酶及其应用。本发明改造腈水合酶的获得方法为:如序列表SEQ ID NO:2所示氨基酸序列的α亚基的133位Pro和如序列表SEQ ID NO:1所示氨基酸序列的β亚基的215位Asp分别置换为Cys,使两个亚基之间形成二硫键。本发明改造腈水合酶的抗逆性、耐热性和产物耐受性都有显著提升,并且没有导致腈水合酶活性的降低。改造腈水合酶可催化获得高浓度丙烯酰胺产物,且可以多批次回用。
Description
技术领域
本发明属于酶工程和工业微生物技术领域,具体涉及一种改造腈水合酶及其应用。
背景技术
微生物生产的腈水合酶可以高效催化丙烯腈水合生成丙烯酰胺。丙烯酰胺聚合产生的聚丙烯酰胺在三次采油、水处理、造纸等工业生产领域具有非常广泛的应用。利用微生物产生的腈水合酶催化生产丙烯酰胺具有一系列优点,包括反应在常温常压下进行、能耗低、操作简单、安全、丙烯腈转化率高、产物浓度和纯度高等,因此逐渐成为丙烯酰胺生产的主要方法。
微生物法生产丙烯酰胺的研究重点在于高产腈水合酶菌株的发现和改造以及对腈水合酶本身性能的基因工程改造。其中,在基因工程方面,日本三菱化成株式会社对来自根瘤菌属的腈水合酶基因和蛋白申请了专利《具有腈水合酶活性的新型蛋白和编码该蛋白的基因》(申请号:93106122.9);三井化学株式会社对来自嗜热假诺卡氏菌JCM3095的腈水合酶的蛋白以及编码它的基因申请了专利《参与活化腈水合酶的蛋白以及编码它的基因》(专利号:ZL99106291.4);《新型腈水合酶》(专利号:02156180.X),并研究了该基因在重组大肠杆菌中的表达;德国底古萨股份公司申请了《红球菌属的腈水合酶》(申请号:200580008206.8);清华大学公开了“一种腈水合酶及其编码基因与应用”,构建了α亚基起始密码子突变的腈水合酶,并在大肠杆菌中高活性表达(专利号:ZL 200410042576.0);清华大学在专利“一种腈水合酶基因簇及其应用”中公开了红色(赤)红球菌RhodococcusruberTH中与腈水合酶高表达相关的结构基因和调控基因序列(专利号:ZL200910076710.1)。
除了产物/底物耐受性外,在微生物法生产丙烯酰胺的催化水合过程中,制约生产效率的另一个主要问题就是产酶细胞的耐热性较差,水合温度必须通过低温制冷剂控制在15-22℃。由于腈水合酶催化丙烯腈水合生成丙烯酰胺是强放热反应,工业生产中控温的冷量经常供应不足,导致水合温度波动到25℃以上。较高的水合温度一方面会加快反应速率,提高生产效率,另一方面则会造成腈水合酶的快速失活,减少反应批次,增加生产成本。日本三菱丽阳株式会社公开了专利《改良型腈水合酶》(公开号:CN 1961072A),对腈水合酶β亚基第93位、第167位和219位氨基酸残基进行定点突变,提高了腈水合酶的热稳定性;清华大学在专利“一种突变腈水合酶”中对腈水合酶β亚基的141位Ser、143位Ser、144位Leu进行置换,使得腈水合酶的耐热性、产物耐受性和超声耐受性都有显著提升(专利号:ZL201110415465X)。
发明内容
本发明为了提高腈水合酶的抗逆性、耐热性和产物耐受性,提出一种改造腈水合酶及其应用。
具体技术方案如下:
一种改造腈水合酶通过将原腈水合酶的β亚基第215位氨基酸和α亚基第133位氨基酸之间形成二硫键改造而成;所述原腈水合酶的α亚基的氨基酸序列如序列表SEQ IDNO:2所示氨基酸序列;所述原腈水合酶的β亚基的氨基酸序列如序列表SEQ ID NO:1所示氨基酸序列。
进一步地,所述二硫键形成的方法为:将SEQ ID NO:1所示氨基酸序列的215位Asp置换为Cys,将SEQ ID NO:2所示氨基酸序列的133位Pro置换为Cys。
一种编码上述改造腈水合酶的基因。
进一步地,所述编码改造腈水合酶的基因序列如SEQ ID NO:3所示。
一种含有所述编码改造腈水合酶基因的表达载体。
进一步地,所述表达载体优选质粒。
进一步地,所述启动子为原核生物启动子,包含但不限于如Pami,Pa2,Ptac,PlacZ启动子(刘昌春等.红球菌启动子识别及β-半乳糖苷酶报告基因表达.生物工程学报,2009,25(9):1360-1365.)。
一种含有所述编码改造腈水合酶基因或含有所述表达载体的转化体。
进一步地,所述转化体的构建方法为:将含有所述编码改造腈水合酶基因直接插入受体菌的染色体,或采用氯化钙法或电穿孔转化法将含有所述编码改造腈水合酶基因的表达载体导入受体菌。
进一步地,所述受体菌为大肠杆菌、红球菌、诺卡氏菌或丙酸棒杆菌。
进一步地,所述转化体在制备丙烯酰胺中的应用。
上述改造腈水合酶在制备丙烯酰胺中的应用。
本发明的有益效果:
1、本发明改造腈水合酶的抗逆性、耐热性和产物耐受性都有显著提升,并且没有导致腈水合酶活性的降低。在60℃高温下浸泡10min,改造后腈水合酶的残留酶活是改造前腈水合酶残留酶活的2.35倍;在高浓度丙烯酰胺溶液的浸泡下,改造后腈水合酶的残留酶活是改造前腈水合酶残留酶活的2.12倍。
2、改造腈水合酶可催化获得高浓度丙烯酰胺产物,并且可以多批次回用。在利用丙烯腈生产丙烯酰胺的过程中,改造后腈水合酶可催化生产62%高浓度丙烯酰胺,而改造前腈水合酶仅可催化生成50%丙烯酰胺;在利用腈水合酶催化生产50%丙烯酰胺的批次反应过程中,改造后腈水合酶可实现连续4批次回用,而改造前腈水合酶仅可用1次,改造后腈水合酶综合性能优势明显,具有良好的工业应用前景。
附图说明
图1为改造前、后腈水合酶的活性比较。
图2为改造前、后腈水合酶的热稳定性比较。
图3为改造前、后腈水合酶的丙烯酰胺耐受性比较。
图4为改造前、后腈水合酶催化丙烯腈生成高浓度丙烯酰胺比较。
图5为改造后腈水合酶SBMDB生产得到的高浓度丙烯酰胺。
图6为改造后腈水合酶催化丙烯腈水合生成丙烯酰胺批次反应中丙烯酰胺浓度变化。
图7为改造后腈水合酶催化丙烯腈水合生成丙烯酰胺批次反应中电导率值变化。
具体实施方式
以下实施例便于更好地理解本发明,但不仅限于此。
以下实验方法如无特殊说明均为常规方法;实验试剂如无特殊说明均可从商业途径获得。
实施例1:改造后腈水合酶SBMDB基因置换过程
(1)以质粒pNV-SBM(陈杰等,耦合末端盐桥与定点突变的重组腈水合酶催化动力学.化工学报,2014,65(7):2821-2828)为模板,采用反向聚合酶链式反应(PCR)方法进行基因突变。首先对腈水合酶SBM的β亚基引入置换Aspβ215Cys。
采用正向引物SBM-beta215-sense:TGTGTAGTGTGCGTCGATCTCTG;反向引物SBM-beta215-anti:TTTCCCGTTTCCGTCGTCG。
PCR反应体系为:
反应条件为:
所得PCR扩增产物利用OMEGA biotek公司生产的E.Z.N.A.Gel Extraction Kit凝胶回收试剂盒回收,回收过程按照说明书所述过程完成。所得DNA片段进行磷酸化反应,磷酸化反应体系为:
反应条件为37℃,30min。
所得磷酸化产物利用OMEGA biotek公司生产的E.Z.N.A.Gel Extraction Kit凝胶回收试剂盒进行纯化,纯化过程按照说明书所述过程完成。纯化片段利用T4 DNA连接酶在4℃进行连接反应16h;再将连接反应产物转化宿主菌E.coli BL21(DE3)的感受态细胞(天根生化科技有限公司),采用卡那霉素抗性(Kan)LB固体培养基平板,挑选阳性克隆,所得重组质粒送铂尚生物科技公司进行DNA测序验证。
LB培养基组成为:蛋白胨10g/L,酵母粉5g/L,氯化钠10g/L,卡那霉素,50mg/L,琼脂粉,15g/L,pH 7.0。
以上述所得重组质粒为模板,继续对腈水合酶α亚基引入置换PROα133Cys。突变方法与上述腈水合酶β亚基引入置换方法相似,采用正向引物为SBM-alpha133-sense:TGTCGTGGAGTGCTCAAGCG,反向引物为SBM-alpha133-anti:GTCTGCTACCACTCGGGACCG。
通过以上基因置换过程,即得到改造后的腈水合酶基因,其具有SEQ ID NO:3所示序列,将其命名为SBMDB。
实施例2:改造后腈水合酶转化体的构建及改造腈水合酶在转化体中的表达
将实施例1获得的改造腈水合酶基因(SEQ ID NO:3所示)的质粒PNV-SBMDB采用电穿孔的方式转入宿主菌红色红球菌R.ruber TH3。转化体采用含卡那霉素浓度为25mg/L的红球菌平板培养基进行筛选,从而得到转化体R.ruber TH3/pNV-SBMDB。
得到的表达菌株R.ruberTH3/pNV-SBMDB进行摇瓶发酵培养。首先在含有25mg/L卡那霉素的红球菌种子培养基中接种,于28℃、200rpm培养36h。
从培养得到的种子液中接种10%至红球菌发酵培养基中,于28℃、200rpm培养48h。所得细胞进行酶活测定。
红球菌平板培养基组成为:葡萄糖10g/L,酵母膏3g/L,NaCl 1g/L,K2HPO4·3H2O2g/L,MgSO4·7H2O 0.2g/L,琼脂15g/L。
红球菌种子培养基组成为:葡萄糖20g/L,酵母膏1g/L,蛋白胨7g/L,K2HPO4·3H2O0.5g/L,KH2PO4 0.5g/L,MgSO4·7H2O 0.5g/L。
红球菌发酵培养基组成为:葡萄糖30g/L,酵母膏7.5g/L,尿素10g/L,K2HPO4·3H2O2.28g/L,KH2PO4 0.866g/L,MgSO4·7H2O 1g/L,谷氨酸钠1g/L,CoCl2 10.4mg/L。
酶活测定以丙烯腈为底物,采用气相色谱法。取4.5mL 10mM pH 7.0的磷酸盐PBS缓冲液和0.1mL的菌液装入10mL EP管中,恒温至28℃,加入200μL丙烯腈后迅速混匀,与此同时,按下秒表计时,准确反应5min后,加入200μL 2.5M HCl终止反应。将反应液离心后,与4%的乙酰胺(内标)溶液等体积混合,采用气相色谱仪Trace1300(Thermo,美国)内标法测量丙烯酰胺浓度。气相色谱操作条件为:聚乙二醇高分子毛细管柱PEG-20M(30m×0.25mm×2μm),进样口为SPL,温度260℃;FID检测器,温度260℃;柱温190℃;载气为氮气,分压为108kPa;分流进样,进样量0.4μL,分流比为50:1。
酶活测定结果表明,重组菌R.ruber TH3/pNV-SBMDB表达改造腈水合酶的酶活为3452U/mL,改造前腈水合酶酶活为3601U/mL(如图1)。改造后腈水合酶酶活仅略有下降。
实施例3:改造后腈水合酶的抗逆性评估
将实施例2中收获的50mL表达菌株R.ruber TH3/pNV-SBMDB细胞(表达改造腈水合酶)与对照菌株R.ruber TH3/pNV-SBM细胞用等体积的去离子水洗涤一次,再重悬于等体积的10mM的PBS缓冲液中。
各取5mL重悬的细胞,在60℃水浴中放置10min。对改造后腈水合酶和改造前腈水合酶的残余酶活进行测定,结果表明,改造后腈水合酶的残留酶活为69.40%,而改造前腈水合酶的残留酶活仅为29.47%。改造后腈水合酶的热稳定性显著提升(如图2)。
各取20mL重悬的重组细胞分别放置于100mL锥形瓶中,边搅拌边滴加丙烯酰胺,60%的丙烯酰胺以0.5mL/min的流速均匀滴加至锥形瓶中。每隔一段时间从锥形瓶中取出1mL混合液离心,所得沉淀用去离子水清洗三次后,测定残余的腈水合酶酶活。当混合液中丙烯酰胺浓度达到40%时,改造后腈水合酶的残留酶活为36%,而改造前的腈水合酶残留酶活仅为17%。改造后腈水合酶的丙烯酰胺耐受性显著提升(如图3)。
实施例4:改造后腈水合酶催化丙烯腈水合生成高浓度丙烯酰胺
将实施例2中收获的表达菌株R.ruber TH3/pNV-SBMDB细胞(表达改造腈水合酶)与对照菌株R.ruber TH3/pNV-SBM细胞用等体积的去离子水洗涤一次,再重悬于等体积的去离子水中。
分别取400mL上述细胞悬浮液放置于1000mL三口瓶中,冰浴条件下进行水合反应。边搅拌边滴加丙烯腈,滴加速度以控制反应温度为18-25℃来调节,当反应体系中丙烯腈浓度高于1%时,停止滴加丙烯腈。如图4所示,改造后表达菌株R.ruber TH3/pNV-SBMDB细胞可催化生成浓度为62%的丙烯酰胺,最终生成的丙烯酰胺由于浓度过高从而产生晶体附着于瓶壁(如图5)。而改造前菌株仅能催化生成浓度为50%的丙烯酰胺。
实施例5:改造后腈水合酶催化丙烯腈水合生成丙烯酰胺批次反应
分别取400mL实施例4中所得的细胞悬浮液放置于1000mL三口瓶中,冰浴条件下进行水合反应。边搅拌边滴加丙烯腈,滴加速度以控制反应温度为18-25℃来调节,当丙烯酰胺产物浓度达到50%时,停止滴加丙烯腈。反应得到的丙烯酰胺通过中空纤维膜与菌体分离,所得菌体回收并继续进行下一批次水合反应,如此重复。反应过程中隔一段时间取样测定反应液中的丙烯酰胺浓度和电导率值。如图6所示,改造后表达菌株R.ruber TH3/pNV-SBMDB细胞可以完成4批反应,而改造前细胞仅能完成1批反应。在该反应过程中,改造后表达菌株R.ruber TH3/pNV-SBMDB细胞电导值也明显低于改造前菌株(如图7)。说明改造后腈水合酶具有更加优良的水合催化效果,所得改造菌株在丙烯腈水合生成丙烯酰胺催化过程中具有更优秀的表现。
SEQUENCE LISTING
<110> 清华大学
<120> 一种改造腈水合酶及其应用
<130> 2017
<160> 3
<170> PatentIn version 3.3
<210> 1
<211> 229
<212> PRT
<213> 人工序列
<400> 1
Met Asp Gly Ile His Asp Thr Gly Gly Met Thr Gly Tyr Gly Pro Val
1 5 10 15
Pro Tyr Gln Lys Asp Glu Pro Phe Phe His Tyr Glu Trp Glu Gly Arg
20 25 30
Thr Leu Ser Ile Leu Thr Trp Met His Leu Lys Gly Met Ser Trp Trp
35 40 45
Asp Lys Ser Arg Phe Phe Arg Glu Ser Met Gly Asn Glu Asn Tyr Val
50 55 60
Asn Glu Ile Arg Asn Ser Tyr Tyr Thr His Trp Leu Ser Ala Ala Glu
65 70 75 80
Arg Ile Leu Val Ala Asp Lys Ile Ile Thr Glu Glu Glu Arg Lys His
85 90 95
Arg Val Gln Glu Ile Leu Glu Gly Arg Tyr Thr Asp Arg Asn Pro Ser
100 105 110
Arg Lys Phe Asp Pro Ala Glu Ile Glu Lys Ala Ile Glu Arg Leu His
115 120 125
Glu Pro His Ser Leu Ala Leu Pro Gly Ala Glu Pro Lys Phe Lys Glu
130 135 140
Gly Asp Lys Val Lys Val Lys Asn Met Asn Pro Leu Gly His Thr Arg
145 150 155 160
Cys Pro Lys Tyr Val Arg Ser Lys Ile Gly Glu Ile Val Thr Ser His
165 170 175
Gly Cys Gln Ile Tyr Pro Glu Ser Ser Ser Ala Gly Leu Gly Asp Asp
180 185 190
Pro Arg Pro Leu Tyr Thr Val Ala Phe Ser Ala Gln Glu Leu Trp Gly
195 200 205
Asp Asp Gly Asn Gly Lys Asp Val Val Cys Val Asp Leu Trp Glu Pro
210 215 220
Tyr Leu Ile Ser Ala
225
<210> 2
<211> 203
<212> PRT
<213> 人工序列
<400> 2
Met Ser Glu His Val Asn Lys Tyr Thr Glu Tyr Glu Ala Arg Thr Lys
1 5 10 15
Ala Ile Glu Thr Leu Leu Tyr Glu Arg Gly Leu Ile Thr Pro Ala Ala
20 25 30
Val Asp Arg Val Val Ser Tyr Tyr Glu Asn Glu Ile Gly Pro Met Gly
35 40 45
Gly Ala Lys Val Val Ala Lys Ser Trp Val Asp Pro Glu Tyr Arg Lys
50 55 60
Trp Leu Glu Glu Asp Ala Thr Ala Ala Met Ala Ser Leu Gly Tyr Ala
65 70 75 80
Gly Glu Gln Ala His Gln Ile Ser Ala Val Phe Asn Asp Ser Gln Thr
85 90 95
His His Val Val Val Cys Thr Leu Cys Ser Cys Tyr Pro Trp Pro Val
100 105 110
Leu Gly Leu Pro Pro Ala Trp Tyr Lys Ser Met Glu Tyr Arg Ser Arg
115 120 125
Val Val Ala Asp Pro Arg Gly Val Leu Lys Arg Asp Phe Gly Phe Asp
130 135 140
Ile Pro Asp Glu Val Glu Val Arg Val Trp Asp Ser Ser Ser Glu Ile
145 150 155 160
Arg Tyr Ile Val Ile Pro Glu Arg Pro Ala Gly Thr Asp Gly Trp Ser
165 170 175
Glu Asp Glu Leu Ala Lys Leu Val Ser Arg Asp Ser Met Ile Gly Val
180 185 190
Ser Asn Ala Leu Thr Pro Gln Glu Val Ile Val
195 200
<210> 3
<211> 1315
<212> DNA
<213> 人工序列
<400> 3
atggatggta tccacgacac aggcggcatg accggatacg gaccggtccc ctatcagaag 60
gacgagccct tcttccacta cgagtgggag ggtcggaccc tgtcgattct gacctggatg 120
catctcaagg gcatgtcgtg gtgggacaag tcgcggttct tccgggagtc gatggggaac 180
gaaaactacg tcaacgagat tcgcaactcg tactacaccc actggctgag tgcggcagaa 240
cgtatcctcg tcgccgacaa gatcatcacc gaagaagagc gaaagcaccg tgtgcaggag 300
atcctcgagg gtcggtacac ggacaggaac ccgtcgcgga agttcgatcc ggccgagatc 360
gagaaggcga tcgaacggct tcacgagccc cactccctag cacttccagg agcggagccg 420
aaattcaaag aaggtgacaa ggtcaaagtg aagaatatga acccgctggg acacacacgg 480
tgcccgaaat atgtgcggag caagatcggg gaaatcgtca cctcccacgg ctgccagatc 540
tatcccgaga gcagctccgc cggcctcggc gacgatcccc gcccgctcta cacggtcgcg 600
ttttccgccc aggaactgtg gggcgacgac ggaaacggga aatgtgtagt gtgcgtcgat 660
ctctgggaac cgtacctgat ctctgcgtga aaggaatacg ataatgagcg agcacgtcaa 720
taagtacacg gagtacgagg cacgtaccaa ggcaatcgaa actttgctgt acgagcgagg 780
gctcatcacg cccgccgcgg tcgaccgagt cgtttcgtac tacgagaacg agatcggccc 840
gatgggcggt gccaaggtcg tggcgaagtc ctgggtggac cctgagtacc gcaagtggct 900
cgaagaggac gcgacggccg cgatggcgtc attgggctat gccggtgagc aggcacacca 960
aatttcggcg gtcttcaacg actcccaaac gcatcacgtg gtggtgtgca ctctgtgttc 1020
gtgctatccg tggccggtgc ttggtctccc gcccgcctgg tacaagagca tggagtaccg 1080
gtcccgagtg gtagcagact gtcgtggagt gctcaagcgc gatttcggtt tcgacatccc 1140
cgatgaggtg gaggtcaggg tttgggacag cagctccgaa atccgctaca tcgtcatccc 1200
ggaacggccg gccggcaccg acggttggtc cgaggacgag ctggcgaagc tggtgagccg 1260
ggactcgatg atcggtgtca gtaatgcgct cacaccccag gaagtgatcg tatga 1315
Claims (10)
1.一种改造腈水合酶,其特征在于,通过将原腈水合酶的β亚基第215位氨基酸和α亚基第133位氨基酸之间形成二硫键改造而成;所述原腈水合酶的α亚基的氨基酸序列如序列表SEQ ID NO:2所示氨基酸序列;所述原腈水合酶的β亚基的氨基酸序列如序列表SEQ ID NO:1所示氨基酸序列。
2.根据权利要求1所述的改造腈水合酶,其特征在于,所述二硫键形成的方法为:将SEQID NO:1所示氨基酸序列的215位Asp置换为Cys,将SEQ ID NO:2所示氨基酸序列的133位Pro置换为Cys。
3.一种编码权利要求1或2所述改造腈水合酶的基因。
4.根据权利要求3所述的改造腈水合酶的基因,其特征在于,所述编码改造腈水合酶基因序列如SEQ ID NO:3所示。
5.一种含有权利要求3所述编码改造腈水合酶基因的表达载体。
6.一种含有权利要求3所述编码改造腈水合酶基因或含有权利要求5所述表达载体的转化体。
7.根据权利要求6所述的转化体,其特征在于,所述转化体的构建方法为:将含有权利要求3所述编码改造腈水合酶基因直接插入受体菌的染色体,或采用氯化钙法或电穿孔转化法将含有权利要求5所述编码改造腈水合酶基因的表达载体导入受体菌。
8.根据权利要求7所述的转化体,其特征在于,所述受体菌为大肠杆菌、红球菌、诺卡氏菌或丙酸棒杆菌。
9.权利要求6-8任一项所述转化体在制备丙烯酰胺中的应用。
10.权利要求1或2所述改造腈水合酶在制备丙烯酰胺中的应用。
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